EP0175322A2 - Membrane rendue hydrophile à base d'un matériau poreux hydrophobe et son procédé de fabrication - Google Patents

Membrane rendue hydrophile à base d'un matériau poreux hydrophobe et son procédé de fabrication Download PDF

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Publication number
EP0175322A2
EP0175322A2 EP19850111687 EP85111687A EP0175322A2 EP 0175322 A2 EP0175322 A2 EP 0175322A2 EP 19850111687 EP19850111687 EP 19850111687 EP 85111687 A EP85111687 A EP 85111687A EP 0175322 A2 EP0175322 A2 EP 0175322A2
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EP
European Patent Office
Prior art keywords
membrane
hydrophilizing agent
water
hydrophobic
propylene glycol
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP19850111687
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German (de)
English (en)
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EP0175322A3 (en
EP0175322B1 (fr
Inventor
Hisayoshi Yamamori
Michio Inoue
Kazuto Kawashima
Hisao Tanaka
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Rayon Co Ltd
Original Assignee
Mitsubishi Rayon Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from JP59194452A external-priority patent/JPS6171803A/ja
Priority claimed from JP59238484A external-priority patent/JPS61118436A/ja
Priority claimed from JP60049140A external-priority patent/JPS61207449A/ja
Application filed by Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Publication of EP0175322A2 publication Critical patent/EP0175322A2/fr
Publication of EP0175322A3 publication Critical patent/EP0175322A3/en
Application granted granted Critical
Publication of EP0175322B1 publication Critical patent/EP0175322B1/fr
Expired legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0081—After-treatment of organic or inorganic membranes
    • B01D67/0088—Physical treatment with compounds, e.g. swelling, coating or impregnation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0081—After-treatment of organic or inorganic membranes
    • B01D67/0095—Drying
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/36—After-treatment
    • C08J9/40—Impregnation
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S521/00—Synthetic resins or natural rubbers -- part of the class 520 series
    • Y10S521/918—Physical aftertreatment of a cellular product
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/249921—Web or sheet containing structurally defined element or component
    • Y10T428/249953—Composite having voids in a component [e.g., porous, cellular, etc.]
    • Y10T428/249978—Voids specified as micro
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/249921—Web or sheet containing structurally defined element or component
    • Y10T428/249953—Composite having voids in a component [e.g., porous, cellular, etc.]
    • Y10T428/249978—Voids specified as micro
    • Y10T428/249979—Specified thickness of void-containing component [absolute or relative] or numerical cell dimension
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/249921—Web or sheet containing structurally defined element or component
    • Y10T428/249953—Composite having voids in a component [e.g., porous, cellular, etc.]
    • Y10T428/249987—With nonvoid component of specified composition

Definitions

  • This invention relates to a hydrophilized membrane of a porous hydrophobic material and a process for preparing such a membrane.
  • porous hydrophobic membranes made of polymer materials, such as polyethylene, polypropylene, polytetrafluoroethylene and copolymers of an olefin monomer and a fluorinated olefin monomer, have been used for water treatment applications, since they are excellent in water resisting property and resistance to chemicals and attacks by bacteria.
  • a membrane is used in medical facilities to obtain germ-free water and also used in a semiconductor manufacturing factory to obtain water of high purity.
  • hydrophobic membranes are porous, water is not allowed to pass through or permeate them, if not subjected to a high pressure. Therefore, such hydrophobic membranes under consideration need to be hydrophilized to allow water to permeate them.
  • Japanese Patent Laid-Open Publication No. 59-501049 discloses a process wherein a porous hydrophobic membrane is hydrophilized by coating the membrane with a mixture of a carbohydrate and a non-ionic ester of an organic monocarboxylic acid, such as a monoester of sorbitan and capric acid, lauric acid, myristic acid, palmitic acid and/or oleic acid.
  • an organic monocarboxylic acid such as a monoester of sorbitan and capric acid, lauric acid, myristic acid, palmitic acid and/or oleic acid.
  • the membrane prepared therethrough has a strong odor to make it undesirable to use the membrane as a filter for a water purifier for drinking use.
  • the water passing through the membrane processed in accordance with this preceding proposal suffers foaming or bubbling due to entrainment of the processing agent.
  • the method of hydrophilizing a porous hydrophobic membrane involves the step of passing a liquid soluble in water and having a low surface tension, such as ethanol, through the pores of the membrane followed by replacing the liquid by water.
  • a liquid soluble in water and having a low surface tension such as ethanol
  • water is allowed to pass through the pores under a relatively small pressure.
  • the hydrophilized hydrophobic membrane is rendered hydrophobic again, and water is not allowed to pass through the pores unless it is not subjected to an extremely high pressure.
  • it when the hydrophobic membrane is hydrophilized with this conventional method, it must be always kept in wet condition to maintain the hydrophilic nature, leading to cumbersome maintenance problem.
  • Another object of this invention is to provide a hydrophilized membrane of a porous hydrophobic material having at least a part of the surface and pores coated with a hydrophilizing agent which is solid at normal temperature and substantially insoluble in water.
  • a further object of this invention is to provide a hydrophilized membrane of a porous hydrophobic material having at least a part of the surface and pores coated with a hydrophilizing agent which is substantially not released in or entrained by the passing water to give bad odor or otherwise to deteriorate the quality of the water passing therethrough.
  • Yet a further object of this invention is to provide a process for preparing such a hydrophilized membrane of a porous hydrophobic material.
  • this invention is directed to a hydrophilized, water permeable, microporous membrane made of a hydrophobic material, said membrane having micropores therethrough, and said membrane having at least a portion of the surfaces thereof coated with a hydrophilizing agent which is solid at about 20 0 C and substantially insoluble in water.
  • the hydrophilizing agent is a monoester of propylene glycol and a higher saturated fatty acid having 12 to 22 carbon atoms (preferably 14 to 22 carbon atoms), such as lauric acid, myristic acid, palmitic acid, stearic acid and behenic acid.
  • One process for hydrophilizing a microporous hydrophobic membrane comprises:
  • Another process for hydrophilizing a microporous hydrophobic membrane comprises:
  • porous hydrophobic membranes having micropores may be used as the matrix hydrophobic membrane for the hydrophilized membrane according to the present invention.
  • the material for the hydrophobic membrane include polyolefins, such as polyethylene, polypropylene and poly-4-methylpentene-l, fluorine-contained polymers such as polyvinylidene fluoride,
  • the porous membrane may have a shape of hollow fiber or may be molded to have a tubular or film shape.
  • a porous hydrophobic membrane may be prepared by molding a film or hollow fiber from a molten mass of a selected hydrophobic polymer material followed by elongation at a relatively low temperature to provide micropores at the interstices of crystallized lamellae, or by molding a membrane from a mixture composed of a first moldable material which is soluble in a certain solvent and a second moldable hydrophobic polymer material which is insoluble in the solvent followed by extraction of the first moldable material with the solvent.
  • the hydrophobic membrane has a porosity ranging within 20 to 90 vol%. If the porosity is less than 20 vol%, the water permeability of the product hydrophilized membrane becomes too low for practical uses. On the contrary, if the porosity is more than 90 vol%, the mechanical strength of the membrane is lowered significantly to lose the integrity of the product hydrophilized membrane.
  • the porous hydrophobic membrane is then treated with a hydrophilizing agent so that the surfaces and pores thereof are at least partially coated with a hydrophilizing agent which is solid at about 20°C and substantially insoluble in water.
  • a hydrophilizing agent which is solid at about 20°C and substantially insoluble in water.
  • substantially insoluble in water means that the hydrophilizing agent has a solubility in water of not more than 0.02 % within the temperature range at which the finished product is used. It is essential that the hydrophilizing agent is solid at a room temperature or the temperature at which the product membrane is used, and that the hydrophilizing agent has a melting point significantly lower than the melting point and softening point of the combined hydrophobic membrane material.
  • the surfaces and pores of the matrix hydrophobic membrane should be coated with the hydrophylizing agent entirely. It has been empirically found that the merit of the invention may be obtained by coating not less than 10% of the surface areas of pores with the hydrophilizing agent of the invention. Preferably not less than 30% and more preferably not less than 50% of the surface areas of pores are covered or coated with the hydrophilizing agent. Of course, the most favorable result is obtainable when the surfaces and surface areas of pores are coated with the hydrophilizing agent in their entireties.
  • the hydrophilizing agent which may be preferably used in the present invention has excellent affinity or compatibility with the combined hydrophobic material for the porous. membrane, and is soluble in a solvent having a low boiling point, such as ethanol.
  • a solvent having a low boiling point such as ethanol.
  • preferable hydrophilizing agent are propylene glycol mono saturated fatty acid esters, such as a monoester of propylene glycol and a higher saturated fatty acid having 12 to 22 carbon atoms.
  • Specific examples of preferred hydrophilizing agent include propylene glycol monolaurate, propylene glycol monomyristate, propylene glycol monopalmitate, propylene glycol monostearate and propylene glycol monobehenate.
  • the most preferable hydrophilizing agent is propylene glycol monostearate. These hydrophilizing agent may be used singly or in combination.
  • matrix microporous membrane of a hydrophobic material is immersed in a solution of a hydrophilizing agent in a solvent having low boiling point, such as ethanol, to allow the hydrophilizing agent to be impregnated in the pores of the membrane.
  • a solvent having low boiling point such as ethanol
  • the membrane is then removed from the solution, and the solvent is evaporated off.
  • the concentration of the hydrophilizing agent contained in the treating solution ranges preferably from about 0.5 to 10%.
  • the solvent may contain water in an amount of not more than 30%, as far as the hydrophilizing agent is uniformly dissolved in the solvent mixed with water.
  • the amount of the hydrophilizing agent adhering to the membrane ranges generally from 1 to 100%, preferably from 10 to 30%, based on the weight of the hydrophobic membrane.
  • the matrix hydrophobic membrane may be hydrophilized to form a hydrophilized membrane which can be used as a satisfactory filter module by the simple immersion-and-evaporation process as aforementioned, it is preferred that the membrane coated with the hydrophilizing agent is then subjected to a thermal treatment.
  • the thermal treatment is effected by heating the membrane to a temperature lower than the temperature at which the membrane starts to shrink thermally and lower than the softening point of the hydrophobic material forming the matrix porous membrane and not lower than the temperature that is lower by 10°C from the melting point of the used hydrophilizing agent.
  • the hydrophilic nature of the finished product membrane is considerably improved by the thermal treatment.
  • the thermal treatment is effected at a temperature higher than the melting point of the used hydrophilizing agent, it suffices that the thermal treatment temperature is not lower than the temperature that is lower by 10°C from the melting point of the used hydrophilizing agent, as described hereinbefore.
  • the reason for such an improvement in hydrophilic nature by the thermal treatment has not been clarified.
  • the following hypothesis has been built up empirically.
  • the molecules of hydrophilizing agent are oriented randomly with the hydrophobic groups or ends of some molecules facing to the hydrophobic membrane while the hydrophilic groups or ends of other molecules facing to the hydrophobic membrane.
  • major portion of the hydrophilizing agent molecules is rearranged so that the hydrophobic groups or ends thereof face to the hydrophobic membrane with the hydrophilic groups or ends being exposed to the exterior surfaces.
  • a polyethylene membrane having cleaned surfaces was immersed in a both containing a 5 wt% propylene glycol monostearate (Melting Point: 45 0 C) in ethyl alcohol for about 3 minutes. After removing from the bath, the membrane was separated into two pieces. One piece was allowed to stand in a thermostatic chamber maintained at 20 0 C for 2 days to remove ethyl alcohol by spontaneous air drying to prepare a first sample which was not subjected to thermal treatment. The other cut piece was held in a hot air drier maintained at 50 0 C for about an hour to remove ethyl alcohol and subjected to thermal treatment concurrently, whereby a second sample subjected to thermal treatment was prepared.
  • a 5 wt% propylene glycol monostearate Melting Point: 45 0 C
  • First and second samples and a control polyethylene film which had not been immersed in the above mentioned bath were wetted by dripping water thereon. It was observed that the water drop was immediately dispersed and the surface was uniformly wetted on the second sample which had been subjected to thermal treatment.
  • the wetting rate of the first sample is relatively low on the surface of the first sample which had been simply coated with the hydrophilizing agent and not subjected to thermal treatment, although the contact angle was considerably smaller than that on the surface of the control polyethylene film which had not been coated with the hydrophilizing agent.
  • the thermal treatment conducted at a temperature approximate to the softening point or approximate to the pre-melt temperature of the hydrophilizing agent.
  • the thermal treatment is effected at a temperature within a range below the temperature that is higher by 20°C from the melting point of the hydrophilizing agent. It suffices that the thermal treatment is effected by heating the membrane coated with the hydrophilizing agent at a selected temperature for about an hour.
  • the microporous membrane made of a hydrophobic material is hydrophilized by a process comprising the step of applying a molten hydrophilizing agent at least a portion of the surfaces of micropores of a hydrophobic membrane.
  • the amount of the hydrophilizing agent applied on the membrane ranges such that a monomolecular layer is applied over the surfaces and the pore surfaces of the membrane, the preferable amount being within 1 to 100 wt%, preferably 10 to 30 wt%, based on the weight of the matrix membrane.
  • the hydrophilizing agent is melted and the molten hydrophilizing agent is then applied on the hydrophobic membrane.
  • any conventional systems including the dip-nip system, funnel system, nozzle spray system, gravure roller coating system and roller coating system, may be employed.
  • the amount of the hydrophilizing agent adhering onto the hydrophobic membrane is varied depending on the viscosity of the molten mass and the application method employed. Accordingly, it is desirous that the application system or method is selected in consideration of the viscosity of the molten hydrophilizing agent used.
  • the dip-nip system and the funnel system are suited for applying a molten hydrophilizing agent having a relatively high viscosity, whereas the nozzle spray system and the roller costing system are suited for applying a molten hydrophilizing agent having a relatively low viscosity.
  • a soft touch squeezer is used so that a thin layer is applied over the matrix membrane.
  • a porous membrane 2 made of a hydrophobic material is drawn from a feed bobbin 1 to contact with a heated roller 3, and then taken up around a take-up bobbin 6.
  • the surface of the roller 3 is applied with a thin film of a molten hydrophilizing agent contained in a container 5 provided with heating means.
  • the porous membrane 2 is coated with a thin film of the molten hydrophilizing agent which is cooled to a temperature below the melting point of the hydrophilizing agent to be solidified before the membrane 2 is taken up around the take-up bobbin 6.
  • a pair of rollers 3 and 4 is used to uniformalize the molten hydrophilizing agent layer, similarly as in a conventional gravure printing system.
  • the hydrophilizing agent is put into the container 5 where it is heated to a pre-set temperature to form a molten mass.
  • the heated roller 3 or 4 has a peripheral portion dipped in the molten mass and rotated at a predetermined speed, so that a thin film of the molten hydrophilizing agent is entrained by the roller 3 or 4.
  • the thin film of the molten hydrophilizing agent is taken up by the membrane to cover the surface thereof.
  • the amount of the hydrophilizing agent adhering onto the surface of the membrane 2 is controlled by changing the transfer speed of the membrane 2 and by changing the circumferential speed of the coating roller 3 or 4.
  • the coating roller 3 or 4 may have an aventurine surface to prevent the membrane 2 from winding around the coating roller.
  • the membrane applied with the hydrophilizing agent it is again preferable to heat the membrane applied with the hydrophilizing agent to a temperature above the melting point of the hydrophilizing agent so that the hydrophilizing agent impregnates deep into a lot of micropores.
  • a liquid treatment device comprising a hollow housing having at least an inlet port for a liquid to be treated and at least one outlet for the liquid permeated was prepared.
  • a liquid treatment device will be hereinafter referred to as a module, and a U shaped bundle of hollow fibers is disposed within the housing will the ends thereof being in liquid communication with the inlet port.
  • each hollow fiber was made of a microporous polyethylene membrane and had an internal diameter of 300 microns, a thickness of 70 microns and a porosity of 65%.
  • the microporous polyethylene membrane was immersed in a 2 wt% solution of propylene glycol monostearate in ethanol at the room temperature for 5 minutes. After removing the membrane from the solution, it was dried under a reduced pressure for 14 hours in a vacuum drier maintained at 50°C. It was found that the thus treated membrane had propylene glycol monostearate in an amount of 15 wt% of the untreated porous membrane. It was also found that more than about 95% of the surface area of the membrane was covered by a propylene glycol monostearate layer.
  • a water filtering module was manufactured by assembling the thus treated membrane with the aforementioned module so that the hollow fibers had a total membrane area of 0.6 m 2 .
  • the water filtering module was connected to a spout of city water, and water was filtered therethrough at a water pressure of 0.5 kg/cm 2 to find that the water permeability was 10.5 liter/min. After passing 20 liter of water through the module, water contained in the module was removed and the module was then dried at 50°C at a reduced pressure for 24 hours. After the completion of removal of water, the once dried water filtering module was again connected to the spout of city water and water was filtered therethrough under the same condition. At that time, the water permeability of the module or fiber was 10.5 liter/min. The filtered water had not odd odor when it was drank.
  • a water filtering module having a total membrane area of 0.6 m 2 was prepared.
  • the module was hydrophilized by flowing an aqueous ethanol (70 wt% of ethanol) therethrough, and then rinsed with water.
  • Water was passed through the thus prepared comparative module under the same condition as in Example 1 to find that the water permeability was 9.8 liter/min.
  • water contained in the module was removed and the module was then dried under the same condition as in Example 1.
  • Water was again passed through the thus dried comparative module under the same condition to find that no water permeated each fiber. The water pressure was then raised to 2 kg/cm 2 , but water could not pass through the membrane.
  • microporous polyethylene membrane was immersed in a 5 wt% solution of propylene glycol monostearate in ethanol at the room temperature for 5 minutes. After removing the membrane from the solution, it was dried under a reduced pressure for about 10 hours in a vacuum drier maintained at 60°C. It was found that the thus treated membrane had propylene glycol monostearate in an amount of 15.8 wt% of the untreated porous membrane. It was found that more than about 95% of the surface area of the membrane was covered by a propylene glycol monostearate film.
  • a water filtering module was manufactured by assembling the thus treated membrane with the aforementioned module so that the hollow fibers had a total membrane area of 0.6 m 2 .
  • the water filtering module was connected to a spout of city water, and water was filtered therethrough at a water pressure of 0.5 kg/cm 2 to find that the water permeability was 11.0 liter/min.
  • water contained in the module was removed and the module was then dried at 60°C at a reduced pressure for 24 hours.
  • the once dried water filtering module was again connected to the spout of city water and water was filtered therethrough under the same condition. At that time, the water permeability of the module or fiber was 11.0 liter/min.
  • microporous polyethylene membrane was immersed in a 5 wt% solution of propylene glycol monostearate in ethanol at the room temperature for 5 minutes. After removing the membrane from the solution, it was dried under a reduced pressure for about 150 hours in a vacuum drier maintained at 35°C. It was found that the thus treated membrane had propylene glycol monostearate in an amount of 16.4 wt% of the untreated porous membrane. It was found that more than about 95% of the surface area of the membrane was covered by a propylene glycol monostearate layer.
  • a water filtering module was manufactured by assembling the thus treated membrane with the aforementioned module so that the hollow fibers had a total membrane area of 0.6 m 2 .
  • the water filtering module was connected to a spout of'city water, and water was filtered therethrough at a water pressure of 0.5 kg/cm 2 to find that the water permeability was 8.7 liter/min.
  • water contained in the module was removed and the module was then dried at 60°C at a reduced pressure for 24 hours.
  • the once dried water filtering module was again connected to the spout of city water and water was filtered therethrough under the same condition. At that time, the water permeability of the module was 8.7 liter/min.
  • microporous polyethylene membrane was immersed in a 5 wt% solution of propylene glycol monostearate in ethanol at the room temperature for 5 minutes. After removing the membrane from the solution, it was dried by air in a thermostat maintained at 20 0 C for about 70 hours to remove ethanol completely. It was found that the thus treated membrane had propylene glycol monostearate in an amount of 16.4 wt% of the untreated porous membrane. It was found that more than about 95% of the surface area of the membrane was covered by a propylene glycol monostearate layer.
  • a water filtering module was manufactured by incorporating thus treated membrane into the aforementioned module so that the hollow fibers had a total membrane area of 0.6'm 2 . Water was passed through the filtering module under the same condition as in Example 1 to find that the water permeability of the module was 3.2 liter/min.
  • Example 5 In contrast thereto, the module of Example 5 was stained evenly and was kept in the condition adapted for further passage of water.
  • each hollow fiber was made of a microporous polypropyrene membrane and had an internal diameter of 200 microns, a thickness of 25 microns and a porosity of 45%.
  • the microporous polypropyrene membrane was immersed in a 5 wt% solution of propylene glycol monostearate in ethanol at the room temperature for 10 minutes. After removing the membrane from the solution, it was dried under a reduced pressure for 14 hours in a vacuum drier maintained at 60 o C. It was found that the thus treated membrane had propylene glycol monostearate in an amount of 17 wt% of the untreated porous membrane. It was also found that more than about 80% of the surface area of the membrane was covered by a propylene glycol monostearate layer.
  • a water filtering module was manufactured by assembling the thus treated membrane with the aforementioned module so that the hollow fibers had a total membrane area of 0.6 m 2 .
  • the water filtering module was connected to a spout of city water, and water was filtered therethrough at a water pressure of 0.5 kg/cm 2 to find that the water permeability was 1.1 liter/min.
  • water contained in the module was removed and the module was then dried at 50 0 C at a reduced pressure for 24 hours.
  • the once dried water filtering module was again connected to the spout of city water and water was filtered therethrough under the same condition. At that time, the water permeability of the module or fiber was 1.1 liter/min.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
EP19850111687 1984-09-17 1985-09-16 Membrane rendue hydrophile à base d'un matériau poreux hydrophobe et son procédé de fabrication Expired EP0175322B1 (fr)

Applications Claiming Priority (6)

Application Number Priority Date Filing Date Title
JP194452/84 1984-09-17
JP59194452A JPS6171803A (ja) 1984-09-17 1984-09-17 多孔質膜
JP59238484A JPS61118436A (ja) 1984-11-14 1984-11-14 疎水性多孔質膜の親水化加工方法
JP238484/84 1984-11-14
JP60049140A JPS61207449A (ja) 1985-03-12 1985-03-12 親水化多孔質膜及び親水化方法
JP49140/85 1985-03-12

Publications (3)

Publication Number Publication Date
EP0175322A2 true EP0175322A2 (fr) 1986-03-26
EP0175322A3 EP0175322A3 (en) 1987-01-28
EP0175322B1 EP0175322B1 (fr) 1989-12-27

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EP19850111687 Expired EP0175322B1 (fr) 1984-09-17 1985-09-16 Membrane rendue hydrophile à base d'un matériau poreux hydrophobe et son procédé de fabrication

Country Status (6)

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US (2) US4663227A (fr)
EP (1) EP0175322B1 (fr)
KR (1) KR900000773B1 (fr)
AU (1) AU570132B2 (fr)
CA (1) CA1275207C (fr)
DE (1) DE3574936D1 (fr)

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WO1995032130A1 (fr) * 1994-05-25 1995-11-30 Carnaudmetalbox Plc Recipients pour produits liquides
EP2060315A2 (fr) 2007-11-15 2009-05-20 DSMIP Assets B.V. Membrane haute performance
CN113209828A (zh) * 2021-05-13 2021-08-06 山东超滤环境科技有限公司 一种抗菌超滤膜及其制备方法

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US5110326A (en) * 1985-07-31 1992-05-05 Celanese Corporation Immobilized liquid membrane
ZA865173B (en) * 1985-07-31 1987-03-25 Celanese Corp Immobilized liquid membrane
US5173415A (en) * 1986-01-20 1992-12-22 Japan Chemical Research Co., Ltd. Process for removal of viruses from solutions of physiologically active substances
AU7357687A (en) * 1986-04-29 1987-11-24 Murex Corp. Diagnostic kit for sexually transmitted diseases
US4881320A (en) * 1987-10-26 1989-11-21 Cts Corporation Method of making vented seal for electronic components and an environmentally protected component
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AU4751285A (en) 1986-03-27
KR900000773B1 (ko) 1990-02-16
EP0175322A3 (en) 1987-01-28
US4663227A (en) 1987-05-05
DE3574936D1 (de) 1990-02-01
AU570132B2 (en) 1988-03-03
CA1275207C (fr) 1990-10-16
EP0175322B1 (fr) 1989-12-27
KR860002285A (ko) 1986-04-24
US4675213A (en) 1987-06-23

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